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Experimental characterization and optimization of multi-channel spiral wound air gap membrane distillation modules for seawater desalination

机译:海水淡化多通道螺旋卷绕气隙膜蒸馏模块的实验表征及优化

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An experimental characterization of the performance of two multi-channel spiral-wound air-gap membrane distillation modules at commercial-scale was carried out for seawater desalination. The only difference between them was the membrane surface areas: 7.2 m(2) and 24 m(2) and thus the length of the channels (1.5 and 5 m respectively). The influence of the main operating parameters (evaporator inlet temperature, condenser inlet temperature and feed flow rate) was quantified. It was observed that the trade-off between productivity and energy efficiency was mostly related to the heat recovery inside the module. This was affected by the operation and also by the design of the modules: the longer the channel, the better the thermal efficiency but the worse the productivity. Empirical models were derived for each module. Optimum values of the three operating parameters to simultaneously maximize permeate flux and minimize specific heat consumption were obtained using surface response methodology (RSM). In the longest module it was possible to find operating conditions that maximize the productivity without losing thermal efficiency, but in the shortest module a compromise had to be found between both.
机译:对海水淡化进行了商业规模的两种多通道螺旋空气间隙膜蒸馏模块的实验表征。它们之间的唯一区别是膜表面积:7.2μm(2)和24 m(2),因此通道的长度(分别为1.5和5 m)。定量了主要操作参数(蒸发器入口温度,冷凝器入口温度和进料流量)的影响。有人观察到生产力和能量效率之间的权衡大多数与模块内的热量回收有关。这受到了操作的影响,并且通过模块的设计,通道越长,热效率越好,但生产率越差。为每个模块导出经验模型。使用表面响应方法(RSM)获得三种操作参数的最佳值以同时最大化渗透通量并最小化特定的热量消耗。在最长的模块中,可以找到在不失热效率的情况下最大化生产率的操作条件,但在最短的模块中,在两者之间都必须在折衷中找到折衷。

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